JPH0253092B2 - - Google Patents

Info

Publication number
JPH0253092B2
JPH0253092B2 JP57125100A JP12510082A JPH0253092B2 JP H0253092 B2 JPH0253092 B2 JP H0253092B2 JP 57125100 A JP57125100 A JP 57125100A JP 12510082 A JP12510082 A JP 12510082A JP H0253092 B2 JPH0253092 B2 JP H0253092B2
Authority
JP
Japan
Prior art keywords
water
solution
monomer
polymerization
acrylic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP57125100A
Other languages
Japanese (ja)
Other versions
JPS5915417A (en
Inventor
Hisao Takeda
Katsutoshi Tanaka
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KYORITSU JUKI KOGYO KENKYUSHO KK
Original Assignee
KYORITSU JUKI KOGYO KENKYUSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by KYORITSU JUKI KOGYO KENKYUSHO KK filed Critical KYORITSU JUKI KOGYO KENKYUSHO KK
Priority to JP57125100A priority Critical patent/JPS5915417A/en
Publication of JPS5915417A publication Critical patent/JPS5915417A/en
Publication of JPH0253092B2 publication Critical patent/JPH0253092B2/ja
Granted legal-status Critical Current

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  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polymerisation Methods In General (AREA)

Description

【発明の詳細な説明】 本発明は安定液の製法に関するものであり、詳
しくは安定液に用いるベントナイトの分散剤とし
て使用可能なポリマーの製法に関するものであ
る。 安定液とはボーリング、連続壁工法等において
土層掘削時に掘削空間に充填し、内圧を高める事
により土層壁の崩壊を防止し、かつ混入する土砂
を液中に保持する目的で使用する液の総称であ
る。 従来ベントナイトの分散剤として用いられてき
たCMCは天然物であり、微生物により分解する
結果腐販により急速に効果を失なう。 腐販した泥水にCMCを追加してもたちまち分
解し効果の回復は望めないため、腐販した泥水は
棄てるほかは無かつた。これを防止するには水溶
性アクリルポリマーの如き微生物分解をうけない
合成物で安定液を調整する事が望ましい。前述の
様に安定液を用いる分散剤は液中に土砂を保持す
るため増粘作用を持つ必要がある。 しかし通常市販されている水溶性アクリルポリ
マーは液中に混入した土砂を凝集させる性質があ
り分散剤として使用できない。 又非常に低分子量のアクリルポリマーは凝集作
用を示さないが増粘作用を持たぬため安定液を用
いる事ができない。 この様な従来の水溶性ポリマーの性質は重合条
件によるものでありレドツクス系あるいはアゾ系
触媒による重合物に共通の性質である。 本発明者はかかる条件を種々検討の結果還元剤
とアゾ系触媒を併用して重合する事により、安定
液に使用可能な増粘作用のある分散剤を製造し得
る事を発見し本発明に到達した。 本発明におけるポリマーが特異的に有効である
理由は不明であるが高分子の分子構造に起因する
ものと考える。 本発明に用いられる水溶性アクリルポリマーと
しては(メタ)アクリル酸と(メタ)アクリルア
ミドのモル比が100:0〜50:50の組成を持ちか
つアクリル酸は60%以上がアミン、アンモニウ
ム、アルカリ金属により中和されアクリル酸塩の
形を取つている事が望ましい。 重合開始の触媒としてはアゾビスイソブチロニ
トリル、アゾビスイソシアノ吉草酸、アゾビスア
ミノジノプロパン等アゾ系触媒が適当であり過硫
酸塩、過酸化水素、有機過酸化物は不適である。
還元剤としては亜硫酸塩、亜硫酸水素塩が最も望
ましい。亜ニチオン酸塩、チオ硫酸塩は性能が劣
り、硫酸第一鉄の如き重金属イオンは効果が無
い。 これら還元剤はモノマー中の溶存酸素を全量消
費する量以上に加えられ、通常モノマー溶液に対
し50〜50000ppmの範囲で所望の粘度となる様に
選ばれる。 重合時のモノマー溶液の濃度は重要でありアク
リルモノマーに対し40〜60重量%の水分量に調整
する事により、重合熱により水分を気化せしめ重
合後乾燥工程を経る事無く粉砕し微細な粉末を得
る事ができる。 得られた粉末に炭酸ソーダの如きアルカリ金属
塩を混合する事により溶解性を向上させる事もで
きる。 水蒸気の輝散に便ならしむるため重合容器は上
部が開放している必要があり、エンドレスベルト
上で重合する事が好結果を与える。 以下実施例により本発明を具体的に説明する。 実施例 1 アクリル酸72gに30%アンモニア水35gを30℃
に冷却しながら混合してモノマー溶液を調整し
AIBN0.7gをアセトン7mlに溶解した液を混合
後、亜硫酸水素ナトリウム2gをアンモニア水8
gに溶解した液を添加混合しただちにテフロンコ
ーテイング浅皿中で重合を行ない乾燥減量9%の
ポリマー乾燥固体を得た。 粉砕後1N食塩水中にポリマー濃度1%に溶解
し回転粘度計にて測定した25℃における粘度は
8.5cpであつた。 紛粉末を試料1とする。 比較例 1 アクリル酸72gに30%アンモニア水43gを30℃
に冷却しながら混合したモノマー溶液を調整し、
AIBN0.7gとドデシルメルカプタン0.07gをアセ
トン7mlに溶解した液を混合後ただちにテフロン
浅皿中に移して重合させ乾燥減量9%、1N食塩
水中1%溶液粘度8.7cpのポリマー乾燥固体を得
た。 本粉末を試料2とする。 実施例 2 アクリルアミド28g、アクリル酸11g、アクリ
ル酸カリウム50g、水26gの混合溶液にアゾビス
アミジノプロパン塩酸塩0.7g亜硫酸水素ナトリ
ウム7mgを水4gに溶解した液を添加混合後ただ
ちにテフロンコーテイング浅皿に移して重合させ
乾燥減量9.5%、1N食塩水中1%溶液粘度8.5cpの
ポリマー乾燥固体を得た。 本粉末を試料3とする。 比較例 2 亜硫酸水素ナトリウムを加えない事以外の条件
は実施例2と同一の条件で重合を行ない乾燥減量
9.5%、1N食塩水中1%溶液粘度9.7cpのポリマー
乾燥固体を得た。 本粉末を試料4とする。 効果試験 水道水700mlをミキサー中で攪拌しながらベン
トナイト42gを加え、3分後に分散剤2%水溶液
10mlを添加し、さらに5分間攪拌を続ける。 一晩静置後スターラーで5分間攪拌をした後フ
アンネル粘性と水量を測定した。 フアンネル粘性の測定はフアンネル粘度計
(500ml/500ml)の秒数、水量はAPI規格過
試験機において3Kg/cm2・30分におけるml数であ
る。 【表】
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a stabilizer, and more particularly to a method for producing a polymer that can be used as a dispersant for bentonite used in the stabilizer. Stabilizing liquid is a liquid used to fill the excavated space during soil layer excavation in boring, continuous wall construction methods, etc., to prevent the collapse of the soil layer wall by increasing the internal pressure, and to retain the mixed earth and sand in the liquid. It is a general term for CMC, which has traditionally been used as a dispersant for bentonite, is a natural product that rapidly loses its effectiveness due to spoilage as a result of being decomposed by microorganisms. Even if CMC was added to the spoiled muddy water, it would decompose immediately and the effect could not be restored, so the only option was to throw away the spoiled muddy water. To prevent this, it is desirable to prepare the stabilizer with a synthetic material that is not subject to microbial decomposition, such as a water-soluble acrylic polymer. As mentioned above, a dispersant using a stabilizing liquid must have a thickening effect in order to retain earth and sand in the liquid. However, commercially available water-soluble acrylic polymers cannot be used as dispersants because they have the property of agglomerating earth and sand mixed into the liquid. Also, very low molecular weight acrylic polymers do not exhibit a flocculating effect, but they do not have a thickening effect, so a stabilizing solution cannot be used. The properties of such conventional water-soluble polymers depend on the polymerization conditions and are common to polymers produced using redox or azo catalysts. As a result of various studies on such conditions, the present inventor discovered that it is possible to produce a dispersant with a thickening effect that can be used in stabilized liquids by polymerizing using a reducing agent and an azo catalyst together, and has developed the present invention. Reached. Although the reason why the polymer in the present invention is specifically effective is unknown, it is thought to be due to the molecular structure of the polymer. The water-soluble acrylic polymer used in the present invention has a composition in which the molar ratio of (meth)acrylic acid and (meth)acrylamide is 100:0 to 50:50, and 60% or more of the acrylic acid is amine, ammonium, or alkali metal. It is preferable that the acrylic acid is in the form of an acrylate that has been neutralized by the acrylate. As a catalyst for initiating polymerization, azo catalysts such as azobisisobutyronitrile, azobisisocyanovaleric acid, and azobisaminodinopropane are suitable; persulfates, hydrogen peroxide, and organic peroxides are not suitable.
Sulfites and hydrogen sulfites are most preferred as reducing agents. Nithionite and thiosulfate have poor performance, and heavy metal ions such as ferrous sulfate are ineffective. These reducing agents are added in an amount greater than enough to consume all of the dissolved oxygen in the monomer, and are usually selected to provide a desired viscosity in the range of 50 to 50,000 ppm relative to the monomer solution. The concentration of the monomer solution during polymerization is important, and by adjusting the water content to 40 to 60% by weight of the acrylic monomer, the water can be vaporized by the heat of polymerization, and it can be pulverized into a fine powder without going through a drying process after polymerization. You can get it. The solubility can also be improved by mixing an alkali metal salt such as soda carbonate with the obtained powder. The polymerization container must be open at the top to allow water vapor to diffuse and diffuse, and polymerization on an endless belt gives good results. The present invention will be specifically explained below using Examples. Example 1 Add 35 g of 30% ammonia water to 72 g of acrylic acid at 30°C.
Prepare the monomer solution by mixing while cooling.
After mixing a solution of 0.7 g of AIBN dissolved in 7 ml of acetone, 2 g of sodium bisulfite was added to 8 ml of ammonia water.
Immediately after adding and mixing the solution dissolved in 10 g, polymerization was carried out in a Teflon-coated shallow dish to obtain a polymer dry solid having a drying loss of 9%. After pulverization, the viscosity at 25℃ was measured using a rotational viscometer after dissolving the polymer in 1N saline solution at a concentration of 1%.
It was 8.5 cp. Let the powder be Sample 1. Comparative example 1 72g of acrylic acid and 43g of 30% ammonia water at 30℃
Adjust the mixed monomer solution while cooling to
Immediately after mixing, a solution of 0.7 g of AIBN and 0.07 g of dodecyl mercaptan dissolved in 7 ml of acetone was transferred to a Teflon shallow dish and polymerized to obtain a dry polymer solid having a loss on drying of 9% and a viscosity of a 1% solution in 1N saline of 8.7 cp. This powder is designated as sample 2. Example 2 A solution prepared by dissolving 0.7 g of azobisamidinopropane hydrochloride and 7 mg of sodium bisulfite in 4 g of water was added to a mixed solution of 28 g of acrylamide, 11 g of acrylic acid, 50 g of potassium acrylate, and 26 g of water. Immediately after mixing, the mixture was placed in a Teflon-coated shallow dish. The polymer was transferred and polymerized to obtain a dry polymer solid having a loss on drying of 9.5% and a viscosity of a 1% solution in 1N saline of 8.5 cp. This powder is designated as sample 3. Comparative Example 2 Polymerization was carried out under the same conditions as in Example 2 except that sodium hydrogen sulfite was not added, and the drying loss was
A 9.5% polymer dry solid was obtained with a 1% solution viscosity of 9.7 cp in 1N saline. This powder is designated as sample 4. Effect test 42g of bentonite was added to 700ml of tap water while stirring in a mixer, and after 3 minutes, a 2% aqueous dispersant solution was added.
Add 10ml and continue stirring for a further 5 minutes. After standing overnight, the mixture was stirred with a stirrer for 5 minutes, and the funnel viscosity and water amount were measured. Funnel viscosity was measured in seconds using a Funnel viscometer (500 ml/500 ml), and the amount of water was measured in ml at 3 kg/cm 2 for 30 minutes using an API standard over-testing machine. 【table】

Claims (1)

【特許請求の範囲】[Claims] 1 アクリル酸とアクリルアミドのモル比が
100:0〜50:50であり、かつアクリル酸の60%
以上がアクリル酸塩の形を取り、全アクリルモノ
マーに対し水分量が40〜60重量%であるモノマー
水溶液に、アゾ系触媒を添加して重合させ、重合
熱により水分を蒸発させて乾燥固体を得るにあた
り、モノマー溶液に対し50〜50000ppmの還元剤
を添加して製造したポリマーを水に溶解する事を
特徴とする安定液調整用分散剤の製造法。
1 The molar ratio of acrylic acid and acrylamide is
100:0 to 50:50 and 60% of acrylic acid
The above is in the form of an acrylate, and an azo catalyst is added to a monomer aqueous solution with a water content of 40 to 60% by weight based on the total acrylic monomer and polymerized, and the water is evaporated by the heat of polymerization to form a dry solid. 1. A method for producing a dispersant for stabilizing liquid preparation, which comprises adding 50 to 50,000 ppm of a reducing agent to a monomer solution and dissolving the produced polymer in water.
JP57125100A 1982-07-20 1982-07-20 Production of dispersant Granted JPS5915417A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57125100A JPS5915417A (en) 1982-07-20 1982-07-20 Production of dispersant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57125100A JPS5915417A (en) 1982-07-20 1982-07-20 Production of dispersant

Publications (2)

Publication Number Publication Date
JPS5915417A JPS5915417A (en) 1984-01-26
JPH0253092B2 true JPH0253092B2 (en) 1990-11-15

Family

ID=14901849

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57125100A Granted JPS5915417A (en) 1982-07-20 1982-07-20 Production of dispersant

Country Status (1)

Country Link
JP (1) JPS5915417A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5213893A (en) * 1990-09-14 1993-05-25 Nippon Shokubai Co., Ltd. Waterproofing agent for cable

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57125098A (en) * 1980-12-16 1982-08-04 Burroughs Corp Mail letter

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57125098A (en) * 1980-12-16 1982-08-04 Burroughs Corp Mail letter

Also Published As

Publication number Publication date
JPS5915417A (en) 1984-01-26

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